EA200200080A1 - METHOD FOR CLEANING A PIPE FROM SOLID PARTICLES OF POLYMER AND A DEVICE FOR ITS IMPLEMENTATION - Google Patents
METHOD FOR CLEANING A PIPE FROM SOLID PARTICLES OF POLYMER AND A DEVICE FOR ITS IMPLEMENTATIONInfo
- Publication number
- EA200200080A1 EA200200080A1 EA200200080A EA200200080A EA200200080A1 EA 200200080 A1 EA200200080 A1 EA 200200080A1 EA 200200080 A EA200200080 A EA 200200080A EA 200200080 A EA200200080 A EA 200200080A EA 200200080 A1 EA200200080 A1 EA 200200080A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- cleaning
- pipe
- valve
- polymer
- pipeline
- Prior art date
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/06—Flash distillation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1812—Tubular reactors
- B01J19/1837—Loop-type reactors
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/382—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it with a rotatable device only
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F6/00—Post-polymerisation treatments
- C08F6/001—Removal of residual monomers by physical means
- C08F6/003—Removal of residual monomers by physical means from polymer solutions, suspensions, dispersions or emulsions without recovery of the polymer therefrom
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F6/00—Post-polymerisation treatments
- C08F6/24—Treatment of polymer suspensions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00026—Controlling or regulating the heat exchange system
- B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
- B01J2208/0007—Pressure measurement
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00539—Pressure
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00761—Discharging
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00769—Details of feeding or discharging
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00823—Mixing elements
- B01J2208/00858—Moving elements
- B01J2208/00867—Moving elements inside the bed, e.g. rotary mixer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00004—Scale aspects
- B01J2219/00006—Large-scale industrial plants
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/00114—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant slurries
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00193—Sensing a parameter
- B01J2219/00195—Sensing a parameter of the reaction system
- B01J2219/002—Sensing a parameter of the reaction system inside the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00211—Control algorithm comparing a sensed parameter with a pre-set value
- B01J2219/00213—Fixed parameter value
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00222—Control algorithm taking actions
- B01J2219/00227—Control algorithm taking actions modifying the operating conditions
- B01J2219/00229—Control algorithm taking actions modifying the operating conditions of the reaction system
- B01J2219/00231—Control algorithm taking actions modifying the operating conditions of the reaction system at the reactor inlet
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00222—Control algorithm taking actions
- B01J2219/00227—Control algorithm taking actions modifying the operating conditions
- B01J2219/00229—Control algorithm taking actions modifying the operating conditions of the reaction system
- B01J2219/00236—Control algorithm taking actions modifying the operating conditions of the reaction system at the reactor outlet
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00191—Control algorithm
- B01J2219/00222—Control algorithm taking actions
- B01J2219/00227—Control algorithm taking actions modifying the operating conditions
- B01J2219/0024—Control algorithm taking actions modifying the operating conditions other than of the reactor or heat exchange system
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/16—Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Dispersion Chemistry (AREA)
- Polymerisation Methods In General (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Cleaning In General (AREA)
Abstract
В заявке описаны способ и устройство для очистки от твердых частиц полимера трубы, которая соединена с циркуляционным реактором. Устройство имеет датчик (441) давления в циркуляционном реакторе (1), установленный на идущем к нему трубопроводе, сообщаемый с ним первый клапан, второй клапан (418), расположенный между трубопроводом (416) и первым источником (412) инертного разбавителя и сообщаемый с трубопроводом (416) в точке, расположенной между циркуляционным реактором (1) и первым клапаном. По сигналу датчика (441) первый клапан закрывается, а второй открывается, обеспечивая поступление в трубу инертного разбавителя в необходимом для ее очистке от твердых частиц полимера количестве и достаточном давлении.Отчет о международном поиске был опубликован 2000.08.31.The application describes a method and apparatus for cleaning solid particles from a polymer pipe that is connected to a circulation reactor. The device has a pressure sensor (441) in the circulation reactor (1) installed on the pipeline coming to it, the first valve communicating with it, the second valve (418) located between the pipeline (416) and the first inert diluent source (412) and communicated with pipeline (416) at the point located between the circulation reactor (1) and the first valve. At the signal of the sensor (441), the first valve closes and the second opens, ensuring that an inert diluent flows into the pipe in the quantity and sufficient pressure necessary for cleaning it from solid polymer particles. An international search report was published on 2000.08.31.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US8041298A | 1998-05-18 | 1998-05-18 | |
PCT/US1999/006102 WO1999047251A1 (en) | 1998-03-20 | 1999-03-19 | Continuous slurry polymerization volatile removal |
Publications (2)
Publication Number | Publication Date |
---|---|
EA200200080A1 true EA200200080A1 (en) | 2002-04-25 |
EA003709B1 EA003709B1 (en) | 2003-08-28 |
Family
ID=22157197
Family Applications (4)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA200200081A EA200200081A3 (en) | 1998-05-18 | 1999-05-18 | METHOD OF OBTAINING POLYMER (OPTIONS) |
EA200001202A EA002729B1 (en) | 1998-05-18 | 1999-05-18 | Continuous slurry polymerization volatile removal |
EA200200079A EA003081B1 (en) | 1998-05-18 | 1999-05-18 | Continuous volatile removal in slurry polymerization |
EA200200080A EA003709B1 (en) | 1998-05-18 | 1999-05-18 | Process for purging polymer solids from conduit and apparatus therefor |
Family Applications Before (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA200200081A EA200200081A3 (en) | 1998-05-18 | 1999-05-18 | METHOD OF OBTAINING POLYMER (OPTIONS) |
EA200001202A EA002729B1 (en) | 1998-05-18 | 1999-05-18 | Continuous slurry polymerization volatile removal |
EA200200079A EA003081B1 (en) | 1998-05-18 | 1999-05-18 | Continuous volatile removal in slurry polymerization |
Country Status (13)
Country | Link |
---|---|
US (1) | US20020182121A1 (en) |
EP (2) | EP1437174B1 (en) |
JP (1) | JP2003526696A (en) |
KR (1) | KR20010071291A (en) |
CN (1) | CN1301788C (en) |
AU (1) | AU755016B2 (en) |
CA (1) | CA2330967C (en) |
DE (1) | DE69918432T2 (en) |
EA (4) | EA200200081A3 (en) |
HK (1) | HK1039295A1 (en) |
SG (1) | SG120088A1 (en) |
WO (1) | WO1999060028A2 (en) |
ZA (1) | ZA200006673B (en) |
Families Citing this family (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6239235B1 (en) | 1997-07-15 | 2001-05-29 | Phillips Petroleum Company | High solids slurry polymerization |
US6815511B2 (en) * | 1997-07-15 | 2004-11-09 | Chevron Phillips Chemical Company, Lp | Continuous withdrawal from high solids slurry polymerization |
US6281300B1 (en) | 1998-03-20 | 2001-08-28 | Exxon Chemical Patents, Inc. | Continuous slurry polymerization volatile removal |
KR100531628B1 (en) | 1998-03-20 | 2005-11-29 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | Continuous slurry polymerization volatile removal |
EP1344563B1 (en) * | 1998-03-20 | 2007-10-03 | Chevron Phillips Chemical Company LP | Continuous slurry polymerisation volatile removal |
US7268194B2 (en) | 1998-03-20 | 2007-09-11 | Exxonmobil Chemical Patents Inc. | Continuous slurry polymerization process and apparatus |
US20020111441A1 (en) | 1998-03-20 | 2002-08-15 | Kendrick James Austin | Continuous slurry polymerization volatile removal |
WO2001005842A1 (en) * | 1999-07-15 | 2001-01-25 | Phillips Petroleum Company | Slotted slurry take off |
DE10118182A1 (en) | 2001-04-11 | 2002-10-17 | Basf Ag | Working up liquid products from polyisobutene production by cationic polymerisation involves flash evaporation to give a liquid containing polyisobutene and a gas phase containing isobutene and inert diluent |
EP1444273B1 (en) * | 2001-11-06 | 2006-10-25 | Chevron Phillips Chemical Company LP | Continuous slurry polymerization volatile removal |
KR20040091644A (en) * | 2002-02-19 | 2004-10-28 | 엑손모빌 케미칼 패턴츠 인코포레이티드 | Continuous slurry polymerization process using a loop reactor |
WO2003074167A1 (en) * | 2002-02-28 | 2003-09-12 | Exxonmobile Chemical Patents Inc. | Continuous slurry polymerization process in a loop reactor |
WO2004027264A2 (en) * | 2002-09-17 | 2004-04-01 | Chevron Phillips Chemical Company Lp | Improved pumping apparatus and process for slurry polymerization in loop reactors |
CN101503483B (en) * | 2002-09-17 | 2012-09-05 | 切夫里昂菲利普化学有限责任公司 | Pumping apparatus and process for slurry polymerization in loop reactors |
JP2007506818A (en) | 2003-09-24 | 2007-03-22 | バーゼル・ポリオレフィン・ゲーエムベーハー | Loop reactors with various diameters for olefin polymerization |
SA04250276B1 (en) | 2003-09-24 | 2009-02-07 | باسيل بوليوليفين جي ام بي اتش | Suspension polymerization with high solids concentrations in a loop reactor |
EP1586590A1 (en) * | 2004-02-13 | 2005-10-19 | Total Petrochemicals Research Feluy | Transfer vessel between flash tank and purge column for recovering polymer solids |
PL1791875T3 (en) | 2004-08-27 | 2013-11-29 | Chevron Phillips Chemical Co Lp | Energy efficient polyolefin producction process |
GB0426057D0 (en) * | 2004-11-26 | 2004-12-29 | Solvay | Chemical process |
GB0426059D0 (en) * | 2004-11-26 | 2004-12-29 | Solvay | Chemical process |
GB0426058D0 (en) | 2004-11-26 | 2004-12-29 | Solvay | Chemical process |
CN100355835C (en) * | 2005-02-02 | 2007-12-19 | 何光临 | High-molecular polymer alloy and its preparation method |
US7615596B2 (en) * | 2005-09-30 | 2009-11-10 | Chevron Phillips Chemical Company Lp | Multiple component feed methods and systems |
US7629421B2 (en) * | 2005-12-21 | 2009-12-08 | Chevron Phillips Chemical Company Lp | Monomer recovery by returning column overhead liquid to the reactor |
EP1825910A1 (en) * | 2006-02-24 | 2007-08-29 | Total Petrochemicals Research Feluy | Method for transforming a loop reactor |
EP2033976A1 (en) * | 2007-09-03 | 2009-03-11 | INEOS Manufacturing Belgium NV | Slurry phase polymerisation process |
EP2376220A1 (en) | 2008-12-18 | 2011-10-19 | ExxonMobil Chemical Patents Inc. | High pressure polymerization process |
CN102686310B (en) * | 2009-12-22 | 2015-07-08 | 埃克森美孚化学专利公司 | Separation vessels for use in polymerization processes and methods for cleaning same |
EP2651982B1 (en) * | 2010-12-17 | 2018-04-11 | Univation Technologies, LLC | Systems and methods for recovering hydrocarbons from a polyolefin purge gas product |
EP3838930B1 (en) * | 2012-03-16 | 2023-06-28 | Ineos Europe AG | Polymerisation process |
US8987390B2 (en) | 2012-12-18 | 2015-03-24 | Chevron Phillips Chemical Company, Lp | Chain transfer agent removal between polyolefin polymerization reactors |
WO2015022025A1 (en) | 2013-08-14 | 2015-02-19 | Ineos Europe Ag | Polymerization process |
US10029230B1 (en) | 2017-01-24 | 2018-07-24 | Chevron Phillips Chemical Company Lp | Flow in a slurry loop reactor |
WO2018194872A1 (en) * | 2017-04-17 | 2018-10-25 | Chevron Phillips Chemical Company Lp | System and method for processing reactor polymerization effluent |
EP3479896A1 (en) | 2017-11-03 | 2019-05-08 | Borealis AG | Polymerization reactor system comprising at least one withdrawal valve |
EP3801802A1 (en) * | 2018-05-31 | 2021-04-14 | Dow Global Technologies LLC | Devolatilizer design |
WO2021050231A1 (en) * | 2019-09-13 | 2021-03-18 | Exxonmobil Chemical Patents Inc. | Processes and apparatus for bimodal slurry polymerization |
US11673975B2 (en) | 2021-08-24 | 2023-06-13 | Chevron Phillips Chemical Company Lp | System and method for improving dump tank purge time |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3293000A (en) * | 1962-10-05 | 1966-12-20 | Phillips Petroleum Co | Withdrawal of solids from a flowing stream comprising a slurry of same |
US3324093A (en) * | 1963-10-21 | 1967-06-06 | Phillips Petroleum Co | Loop reactor |
FR1585028A (en) * | 1968-05-14 | 1970-01-09 | ||
DE2212611B2 (en) * | 1972-03-16 | 1977-08-04 | BUhler-Miag GmbH, 3300 Braunschweig | DEVICE FOR CONTINUOUS FORMATION OF GOOD PORTIONS AND INTRODUCING THEM INTO A PNEUMATIC CONVEYOR LINE |
DE2409839C2 (en) * | 1974-03-01 | 1982-11-18 | Basf Ag, 6700 Ludwigshafen | Process for producing small-particle olefin polymers |
US4121029A (en) * | 1976-12-06 | 1978-10-17 | Phillips Petroleum Company | Polyolefin reactor system |
US4395523A (en) * | 1978-03-16 | 1983-07-26 | Chemplex Company | Method of making and recovering olefin polymer particles |
US4303771A (en) * | 1978-12-14 | 1981-12-01 | Union Carbide Corporation | Process for the preparation of high density ethylene polymers in fluid bed reactor |
US4461889A (en) * | 1980-09-17 | 1984-07-24 | Phillips Petroleum Company | Separation of solid polymers and liquid diluent |
US4424341A (en) * | 1981-09-21 | 1984-01-03 | Phillips Petroleum Company | Separation of solid polymers and liquid diluent |
US4690804A (en) * | 1983-07-15 | 1987-09-01 | Phillips Petroleum Company | Catalyst feed system |
US4613484A (en) * | 1984-11-30 | 1986-09-23 | Phillips Petroleum Company | Loop reactor settling leg system for separation of solid polymers and liquid diluent |
US5183866A (en) * | 1989-08-30 | 1993-02-02 | Phillips Petroleum Company | Polymer recovery process |
US5565175A (en) * | 1990-10-01 | 1996-10-15 | Phillips Petroleum Company | Apparatus and method for producing ethylene polymer |
US5575979A (en) † | 1991-03-04 | 1996-11-19 | Phillips Petroleum Company | Process and apparatus for separating diluents from solid polymers utilizing a two-stage flash and a cyclone separator |
US5229480A (en) * | 1992-09-03 | 1993-07-20 | E. I. Du Pont De Nemours And Company | Vinyl fluoride polymerization |
US5558472A (en) * | 1993-10-07 | 1996-09-24 | Sumitomo Chemical Company, Limited | Method and apparatus for transporting particles |
US6239235B1 (en) * | 1997-07-15 | 2001-05-29 | Phillips Petroleum Company | High solids slurry polymerization |
-
1999
- 1999-05-18 EA EA200200081A patent/EA200200081A3/en unknown
- 1999-05-18 AU AU40858/99A patent/AU755016B2/en not_active Ceased
- 1999-05-18 EP EP04007088A patent/EP1437174B1/en not_active Revoked
- 1999-05-18 EA EA200001202A patent/EA002729B1/en not_active IP Right Cessation
- 1999-05-18 DE DE69918432T patent/DE69918432T2/en not_active Expired - Fee Related
- 1999-05-18 JP JP2000549646A patent/JP2003526696A/en not_active Withdrawn
- 1999-05-18 CN CNB998063274A patent/CN1301788C/en not_active Expired - Lifetime
- 1999-05-18 SG SG200301298A patent/SG120088A1/en unknown
- 1999-05-18 WO PCT/US1999/011007 patent/WO1999060028A2/en not_active Application Discontinuation
- 1999-05-18 EA EA200200079A patent/EA003081B1/en not_active IP Right Cessation
- 1999-05-18 EP EP99924333A patent/EP1080116B2/en not_active Expired - Lifetime
- 1999-05-18 EA EA200200080A patent/EA003709B1/en not_active IP Right Cessation
- 1999-05-18 CA CA002330967A patent/CA2330967C/en not_active Expired - Fee Related
- 1999-05-18 KR KR1020007012951A patent/KR20010071291A/en not_active Application Discontinuation
-
2000
- 2000-11-16 ZA ZA200006673A patent/ZA200006673B/en unknown
-
2001
- 2001-12-28 HK HK01109167A patent/HK1039295A1/en not_active IP Right Cessation
-
2002
- 2002-05-14 US US10/147,219 patent/US20020182121A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
WO1999060028A2 (en) | 1999-11-25 |
EP1437174B1 (en) | 2011-10-05 |
WO1999060028A3 (en) | 2000-08-31 |
HK1039295A1 (en) | 2002-04-19 |
EP1080116A2 (en) | 2001-03-07 |
DE69918432D1 (en) | 2004-08-05 |
EP1080116B1 (en) | 2004-06-30 |
EP1080116B2 (en) | 2012-10-03 |
EA200200081A3 (en) | 2002-10-31 |
EA200200079A1 (en) | 2002-06-27 |
EA200200081A2 (en) | 2002-06-27 |
AU4085899A (en) | 1999-12-06 |
EP1437174A2 (en) | 2004-07-14 |
DE69918432T2 (en) | 2005-08-04 |
EA003709B1 (en) | 2003-08-28 |
EA002729B1 (en) | 2002-08-29 |
EA200001202A1 (en) | 2001-06-25 |
CN1302225A (en) | 2001-07-04 |
EA003081B1 (en) | 2002-12-26 |
US20020182121A1 (en) | 2002-12-05 |
CA2330967C (en) | 2009-07-28 |
AU755016B2 (en) | 2002-11-28 |
EP1437174A3 (en) | 2004-11-10 |
ZA200006673B (en) | 2001-12-18 |
KR20010071291A (en) | 2001-07-28 |
CA2330967A1 (en) | 1999-11-25 |
JP2003526696A (en) | 2003-09-09 |
CN1301788C (en) | 2007-02-28 |
SG120088A1 (en) | 2006-03-28 |
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Legal Events
Date | Code | Title | Description |
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MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): AM AZ BY KZ KG MD TJ TM |
|
MM4A | Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s) |
Designated state(s): RU |